Preparation of gel-filled separation columns

ABSTRACT

A method of preparing a microcapillary gel separation column for electrophoresis comprises: pretreatment of a tube with a bifunctional reagent to provide polymer bonding sites on the inner wall of the tube; filling the tube with a monomer solution a cross-linking agent, and a photoinitiator; forming a polymer plug by illuminating an initiation section of the tube; growing the plug by moving the tube gradually past the illumination source; and stopping tube motion when the desired length of gal is attained. Provision is made for monitoring polymerization and adjusting tube movement speed to avoid gaps in the growing polymer.

CROSS REFERENCE TO RELATED APPLICATION

This is a division of application Ser. No. 07/538,348, filed Jun. 14,1990, now U.S. Pat. No. 5,061,355.

BACKGROUND OF THE INVENTION

The present invention relates to analytical chemistry and, moreparticularly, to the preparation of gel columns such as those used ingel electrophoresis. A major objective of the present invention is theformation of a gel column which resists migration of the gel from itscontainer and is essentially free of voids.

Much of recent progress in biotechnology, which holds great promise foradvancing medicine and our understanding of life, is predicated on theability to analyze the constituents of living organisms. In many casesit is necessary to separate constituents, e.g., proteins, to identifythem and determine their relative concentrations in a sample.

Gel-column electrophoresis is one important separation methodology.During electrophoresis, an ionic sample is introduced at one end of agel-filled column. The ionized components migrate longitudinally towardthe other end of the column under the influence of an appliedlongitudinal electric field. The rate of migration for a ion is afunction of its charge and bulk. Different chemical species arecharacterized by different bulks and charges so that they migrate atdifferent rates. Since different species migrate at different rates,they can separate into distinct bands along the column.

The different species can be identified in several ways. In some cases,the final position within the column suffices to identify the chemicalspecies. Similarly, species can be identified by the time at which bandselute from the column. In other cases, the chemical composition of theseparated bands can be assessed by a technique such as spectrometry.Alternatively, the gel can be sliced and the bands subject to moreintensive analysis.

Gel columns are typically formed by polymerizing a monomer solution in afused silica tube. The inner wall of the tube is preferably pretreatedwith a bifunctional reagent. One functional group is capable of bondingto the wall, while the other remains available as a bonding site for thegel. Once the tube is so prepared, monomer solution is introduced andpolymerization initiated. The resulting gel is securely bonded to thetube. This bonding resists migration of the gel from the tube duringelectrophoresis due to charges in the gel from impurities or paritallyhydrolyzed monomer functional groups. In addition, bonding minimizes theformation of non-sieving holes near the tube wall that can otherwiseoccur due to shrinkage that accompanies polymerization. However,shrinkage during polymerization can create voids in the form of airbubbles in the interior of the gel when the bifunctional reagentprevents the gel from separating from the tube wall. These voids disturbthe electric fields and the migration of ions through the column,impairing separation.

Precompressing the monomer solution to a density about that of thecompleted gel prevents shrinkage during polymerization and thus thevoids induced by the shrinkage, as taught by Bente and Myerson in U.S.Pat. No. 4,810,456. However, it can be difficult to work with thepressures, preferably around 8200 pounds per square inch, required forprecompression. Furthermore, the resulting columns are subject toforming gel inhomogeneities or voids under application of moderateelectric field strengths, e.g., 200 volts/centimeter, that can be usedduring microcapillary gel electrophoresis.

Another approach to forming void-free gel columns involves adding ahydrophillic polymer to the primary monomer solution, as disclosed byKarger et al. in U.S. Pat. No. 4,865,707. The rationale is that theresulting gel is more elastic and therefore more able to accommodate thestresses induced due to polymer shrinkage. However, the admixedhydrophillic polymer can adversely affect constituent separation duringelectrophoresis. Moreover, this approach has not reliably producedeffective separation columns.

What is needed is an improved method and system for preparingelectrophoretic gel columns. The method should not require the additionof foreign polymer components which adversely affect gel separationproperties. Extreme pressures and other extreme ambient conditionsshould not be required. The resulting gel should be free of voids andshould resist migration even when the higher voltages used formicrocapillary electrophoresis are applied.

SUMMARY OF THE INVENTION

In accordance with the present invention, gel formation progressesgradually along the length of a structure, such as a tube, which definesa longitudinally extending channel. The tube is pretreated to promotebonding of the gel-to-be-formed to the inner wall of the tube. Asubstance including a gel precursor, typically, a monomer solution, isintroduced into the tube. A polymer structure, herein called a "plug",is formed or otherwise positioned within an initiation section of thetube. This sections extends only a fraction of the length of the tube,the remainder of the tube remaining essentially devoid of polymer atthis point. The plug is then grown to extend over the desired length ofthe tube. "Growth" herein is used in the sense that it used with respectto crystal growth.

This method can be practiced using a system which comprises a light, orother energy source, and means for moving a tube relative to this light.The tube is pretreated and filled with a monomer solution which includesa photoinitiator, such as riboflavin. The light is directed into thetube near one of its ends until polymer begins to form. Afterpolymerization has begun within the selected section, the tube is movedrelative to the light to that polymerization can proceed toward the farend of the tube. Movement is stopped once the desired length of gel isobtained.

Tube movement must not exceed the rate at which the original polymerplug can grow. Otherwise, the "polymer front", i.e., the boundarybetween the polymer and monomer will fall behind the illuminated region,which moves relative to the tube. In this event, the illuminated regioncontains only monomer; when polymerized a second gel plug is formedwhich is separated from the original plug by monomer solution. When themonomer solution in the gap between the gel plugs eventuallypolymerizes, shrinkage occurs which cannot be relieved by drawing inmonomer solution. Accordingly voids can be formed between the locationswhere plugs were formed.

Accordingly, the system can include a polymerization monitor whichmonitors polymerization in a portion of the tube that has recentlypassed the light source. Readings from the monitor are used by acontroller to regulate tube speed.

The present invention provides a variety of systems and methods forforming a gel column. The common ingredient is polymerization whichprogresses longitudinally from a polymer structure in an initiationsection of a channel. The progress can be unidirectional, from one endof the tube to the other, or bidirectional, from the middle toward bothends.

Thus a void-free gel column is prepared without using extreme pressuresor other extreme conditions. Moreover, empirical tests indicate thatcolumns prepared in accordance with the present invention withstand muchgreater field strengths than those prepared using precompression. Inparticular, field strengths as high as 1000 volts/centimeter have beenapplied without causing gel migration from a microcapillary tube. Theseand other features and advantages of the present invention are apparentfrom the description below with reference to the following drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a flow chart of a method in accordance with the presentinvention.

FIG. 2 is a flow chart of a particular implementation of the method ofFIG. 1.

FIG. 3 is a schematic plan view of polymerization system in accordancewith the present invention.

FIG. 4 is a schematic elevational view of parts of the system of FIG. 3.

FIG. 5 is a schematic elevational view of the base of a mount of thesystem of FIG. 3.

FIG. 6 is a schematic plan view of an alternative polymerization systemin accordance with the present invention.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

In accordance with the present invention, a method 100 of preparing amicrocapillary gel electrophoretic column comprises the steps shown inFIG. 1. The inner wall of a capillary tube is prepared, at step 101, sothat a gel to be formed can bond thereto. The tube is filled withmonomer solution of step 102. Polymerization is initiated at an"initiation" section of the tube at step 103. A polymer structure isthen grown from the initial polymer structure, herein called a "plug",along the length of the tube, at step 104. Promotion of polymerizationis stopped, at step 105, when the desired length of gel has been formed.Optionally, polymer growth can be monitored, at step 106 during step104. If the polymerization is not taking place at an optimal rate, asuitable growth parameter can be adjusted, at step 107.

A specific implementation of method 100 is presented as method 200 inFIG. 2. At step 201, a bifunctional reagent is applied to the tube wallsto provide bonding sites for the gel. The tube is filled, at step 202,with monomer solution including acrylamide, bisacrylamide crosslinker,and riboflavin, a photoinitiator. The solution is exposed to nearultraviolet light at step 203. The light is applied to a smallinitiation section of the overall tube. This section is toward one endof the tube. The light causes a polymer structure to form only in thissection.

The tube is moved relative to the light source in step 204. Thispromotes polymerization outside of the initiation section. However,polymerization occurs in a spatially ordered manner from the initiationsection and longitudinally along the tube. Furthermore, polymerizationpreferentially involves covalent bonding with the preexisting plug.Consequently, the initial plug grows so that the polymer front remainsadjacent the light source. Once polymerization has occurred over thedesired length of tube, tube motion can be stopped, as indicated at 205.

Optionally, polymer growth can be monitored at step 206. A light sourcecan be transmitted through the tube behind the polymer front. Anappropriate detector can be used to determine the intensity of lighttransmitted through the tube. The polymer scatters more light than themonomer so that intensity falls as polymerization occurs. Thus, thedetected intensity corresponds to the degree of polymerization. Ifpolymerization is occurring too slowly, the motion of the tube can beslowed to ensure gradual progression of the polymerization.

Method 200 is practiced using system 300 which comprises aphotoinitiation subsystem 302, a polymerization monitor subsystem 304,and a mechanical subsystem 306. Mechanical subsystem 306 provides formoving a fused silica tube 11 relative to photoinitiation subsystem 302and polymerization monitor subsystem 304. Photoinitiation subsystem 304initiates polymerization of monomer solution 13 contained within tube11. The polymerization causes a polymer plug 15 to grow as tube 11 ismoved. Polymerization monitor subsystem 304 monitors the degree ofpolymerization within tube 11 so that a controller 308 can regulate therate at which tube 11 moves to optimize throughput and gel quality.

During gel formation, tube 11 is supported between a first reservoir 17and a second reservoir 19. Reservoirs 17 and 19 contain water to preventevaporation of water from the tube, i.e., drying of the gel. Tube 11extends into each reservoir though respectively included silicone rubbersepta. Tube 11 and reservoirs 17 and 19 define a tube assembly 21 whichis essentially a rigid structure.

Mechanical subsystem 306 comprises a track 310, a rail 312, a rack 314,a pinion 316, and a motor 318. When motor 318 is driven, it rotatespinion 316, which is rigidly coupled to the motor's shaft 320. Pinion316 engages rack 314, forcing translational movement. Rack 314 isrigidly bonded to rail 312. Thus, from the perspective of FIG. 3,clockwise rotation motor 318 causes rail 312 to move to the left.

The purpose of the leftward movement is to pass the contents of tube 11sequentially past beams of light (electro-magnetic radiation) providedby photoinitiation subsystem 302. Photoinitiation subsystem 302comprises a mercury arc lamp 322, a collimating lens 324, a fibercoupler 326, and a pair of optical fibers 328. Optical fibers 328 areheld together at their inputs at fiber coupler 326 so they function as atwo-fiber optical bundle. The output ends of fibers 328 are locked inposition relative to track 310 using fiber optic mount 330. The fiberoutputs are secured by mount 330 so that they direct opposing lightbeams into the adjacent section of tube 11. Thus, leftward longitudinalmovement of tube 11 causes light beams from fibers 328 to scan thecontexts of tube 11 from left to right.

Mechanical subsystem 306 includes stops 332 to prevent tube assembly 21from moving rightward relative to rail 312, while the latter is movingleftward. This could otherwise occur if tube 11 drags against mount 330.Mechanical subsystem 306 also includes a microswitch 334 which detectswhen rail 312 reaches the left end of track 310. A detection is conveyedto controller 308, which then turns off mercury lamp 322 and motor 318.

Initially, tube 11 is filled with monomer solution. Rail 312 and tubeassembly 21 are initially at their rightmost positions. Photoinitiationsubsystem 302 is activated to initiate polymerization near the left endof tube 11 so that a polymer "seed" or "plug" is formed. Leftwardmovement of tube 11 causes polymerization to the right of the plug. Thespeed of motor 318 is set by controller 308. Movement of tube 11 shouldbe fast enough for reasonable throughput and to avoid spontaneouspolymerization to the right of mount 330. Tube 11 should movesufficiently slow that monomer gaps longitudinally between polymersections are minimized. The result should be that polymerization occursas growth of the plug.

While the speed of motor 318 can be predetermined based on trial anderror, system 300 provides for closed loop control of the relativemovement of tube 11 and photoinitiation source 302. Polymerizationmonitor subsystem 304 comprises a tungsten lamp 340, a collimating lens342, a fiber optic coupler 344, a transmission optical fiber 346, areception optical fiber 348, a filter 350 and a photosensor 352.Tungsten emits broadband light which is collimated by lens 342. Thecollimated light is coupled into the input end of fiber 346 via opticalcoupler 344. The output of transmission fiber 346 is secured by mount330 at a position to the left or "downstream" of the longitudinalposition of the outputs of source fibers 328. The input of receptionoptical fiber 348 is held by mount 330 at a position opposite that ofthe output of transmission optical fiber 346. Filter 350, which includesa silicon photodiode, selects out light at wavelengths, around 600nanometers and filters out stray light from the mercury lamp 322.

The polymer form of the polymerizable substance in tube 11 scatters morelight than does the monomer form. Accordingly, the intensity of thelight detected by sensor 352 decreases with polymerization. Controller308 can access the output of sensor 352, and decrease the speed of motor318 when too little polymerization is occurring, and to increase thespeed when polymerization is progressing faster than desired.

System 300 provides for spatially-ordered progressive polymerization.Polymerization occurs as growth at a polymer "front" which tracks thelocation of the photoinitiation source. This is distinct from prior art"monolithic" gel formation approaches in which polymerization can occurat essentially random positions along the tube. In the prior art,monomer can be left between polymer plugs, both of which try to draw themonomer toward them. The polymer that forms from this monomer is almostinevitably under tension which can result in shrinkage voids.

In the present method, polymerization occurs as growth of a plug.Shrinkage due to polymerization simply draws remaining monomer towardthe plug. The tension that could otherwise cause shrinkage voids haslittle opportunity to accumulate. The end result of the method is acolumn that has a gel with negligible tension on the polymer molecules.Thus, shrinkage voids are minimized.

Tube 11 is a 30 centimeter (cm) long fused silica capillary with aninternal diameter of 100 μm and an outer diameter of 300 μm. Polyimidecoating as been burned off except for two centimeters at each end of thetube. The remaining polyimide provides strength where the tube endsextends through the silicone rubber septa of reservoirs 17 and 19.

Tube 11 is pretreated with a bifunctional reagent. This reagent bonds tothe inner walls of tube 11 and, in turn, provides bonding sites forpolymers. The purpose of the bifunctional reagent is to ensure that thegel-to-be-formed resists migration from the tube when an electricpotential is applied during electrophoresis. The bifunctional reagentalso minimizes the presence of non-sieving holes near the inner tubewall.

The pretreatment involves filling tube 11 with a 1% by volume solutionof 3-acryloxypropyltricholoro silane in toluene. Filling capillary tube11 is effected by drawing a vacuum from one end while the other end isinserted into the contents-to-be. Tube 11 with a septum attached at oneend is simply attached to bottles containing the different fluids to bedrawn into the capillary. The reagent is allowed to sit for about tenminutes. Tube 11 is then washed with toluene for five minutes, and thenwith methanol for five minutes. Tube 11 is then air dried for fiveminutes.

After pretreatment, tube 11 is filled with monomer solution and isinserted though a base 460 of mount 330 via a hole 462, best seen inFIG. 4. Hole 462 has cones at either end, as shown in FIG. 5, to aid incapturing tube 11 during insertion. This hole has an inner diameter of500 μm. Septa are place on both ends of tube 11 and then forced intotheir respective reservoirs 17 and 19. This completes tube assembly 21,as shown in FIG. 3.

The monomer solution includes monomer, a crosslinking agent, a chemicalphotoinitiator, and a buffer. The concentrations of monomer andcrosslinking agent are selected to achieve a desired porosity in thefinal gel. These concentrations can be expressed respectively as %T and%C where ##EQU1## The monomer solution used in tube 11 is 10 %T and 2.6%C. The concentration of riboflavin is about 10⁻⁵ molar (M). Whenriboflavin molecules absorb photons of the near ultraviolet wavelengths(400-500 nanometers) emitted by mercury lamp 322, they are excited andbecome free radicals. The free radicals initiate polymerization both bydirectly interacting with monomer and by generating intermediateradicals from water molecules. The buffer is 2 millimolar sodiumphosphate pH 7 buffer. A catalyst, such as TEMED(tetraethylenemethylenediamine) can be added to facilitatepolymerization, provided polymerization remains gradual.

The vacuum is removed and the free end inserted through another septumwhich is fitted snuggly into the top of reservoir 17 which containswater. The reservoir containing monomer is replaced with reservoir 19containing water.

Once tube assembly 21 is in place, a cap 464 for mount 330 is screwedon; i.e., a screw is engaged within countersunk hole 466 in cap 464 andthreaded hole 467 in base 460, shown in FIG. 5. Optical fibers 328 frommercury lamp 322 are inserted in lateral holes 468 on either side of cap464. Each fiber 328 is inserted until it touches tube 11. Then the fiberis withdrawn until light can be seen between tube 11 and the fiber whenlooking down capillary hole 462. This procedure should yield a spacingof about 0.2 to 0.5 millimeters between tube 11 and fibers 328. Fibers328 have a core of about 600 μm. The fibers are sheathed in stainlesssteel for rigidity and have an outer diameter of about 1500 μm. Holes462 have inner diameters of about 1800 μm. For each fiber 328, once thedesired spacing has been achieved, it is held in place by tightening ascrew disposed in a respective hole 470 in cap 464. Sensor fibers 346and 348 are similarly installed using holes in cap 464 two to tenmillimeters downsteam (left in FIG. 3, toward the reader in FIG. 4) ofthose used for fibers.

As indicated in FIG. 4, base 460 of mount 330 extends through an 18 cmelongated slot 472 in rail 312. Slot 472 is at least as long as thedesired length of the eventual gel column. In this case, a 15 cm gelcolumn is to be formed from thirty-inch tube 11. Rail 312 is seatedwithin a square groove 474 of track 310. Rail 112 has a V-shaped groove476 to accommodate tube 11. Rack 314 is metal, while track 310, rail312, and pinion 316, of FIG. 3, are polycarbonate.

Rail 312 begins at its rightmost travel position, with reservoir 17 justto the left of mount 330, from the perspective of FIG. 3. Mercury lamp322 remains on until polymerization is established in the section oftube 11 near the output ends of fibers 328. Polymerization can bepresumed by the passage of a certain amount of time, or detectedvisually or using monitor subsystem 304. Once polymerization has begun,motor 318 can drive tube 11 to the left at a rate selected or controlledto promote gradual growth at the polymer plug front which is advancingrightward relative to tube 11 and is preferably stationary relative tomount 330.

Once the middle 18 cm of tube 11 are exposed to photoinitiation, asindicated by activation of microswitch 334, controller 308 switchesmercury lamp 322 and motor 318 off. Tube 11 is left in place forsufficient curing to take place so that the column can be handledwithout disturbing the gel. Once curing is complete, about 7.5 cm arecut from either end of tube 11 to yield the desired gel filled column.

An alternative system 600 for preparing a microcapillary gelelectrophoretic column, shown in FIG. 6, uses heat rather than light toinitiate polymerization. System 600 is a modification of system 300 solike parts are assigned like reference numerals. A thermal initiationsub system 602 replaces photoinitiation subsystem 302. Removedcomponents include mercury lamp 322, source collimating lens 324, fibercoupler 326, and source fibers 328. In their place are a power supply622, a nichrome resistive heating element 624, and leads 628 betweenpower supply 622 and heating element 624. A modified mount 630 is usedto accommodate leads 628 and heating element 624. In addition, a peltiercooling element 678 leads heating element 624 along tube 11 to minimizepolymerization due to conduction of heat to the right of heating element624.

The monomer solution can be similar except that a thermal initiatorrather than a photoinitiator is used. A 10⁻² to 10⁻⁴ molar concentrationof ammonium persulfate is used in place of the riboflavin used withsystem 300. Once again, a catalyst such as TEMED can be added toincrease the rate of polymerization if desired.

The present invention provides for a variety of alternatives to theembodiments described above. Tubes of different inner diameters areprovided for. For example, the invention applies to the manufacture ofmicrocapillary columns with inner diameters between 25 μm and 500 μm. Inaddition, it can apply to non-capillary columns with diameters between0.5 to 5.0 mm. Other column inner diameters can also be accommodated.Moreover, different lengths are provided for. The invention provides forcolumns 50 mm to 500 mm long.

The method can be applied to any elongated means for defining a channelin which gel is to be formed. Some embodiments prepare elongated groovesand plates with gels. Column cross sections which are square,rectangular, flat, circular and other shapes are within the scope ofthis invention. The resulting product can be used for electrophoresis orother applications for elongated structures with gels. Preparation ofthe channel can involve binding bifunctional reagents, which, as usedherein, include reagents with two or more functional groups. Whereappropriate, the preparation can involve cleaning or abrading a channelwall.

In the preferred embodiments, a monomer served as the precursor for thegel. However, the precursors need not be monomers nor need they be insolution. Oligomer precursors are utilizable, for example. Generally,the tube should be filled with a substance bearing a polymerizable gelprecursor.

As indicated above, photoinitiation and thermal initiation can be usedto begin polymerization. Other forms of energy can also be usedincluding X-rays, gamma rays, particle rays, magnetic fields,ultrasound, etc. A chemical responsive to the form of energy used can beused as an intermediate radical source, just as riboflavin is used inphotoinitiation. Alternatively, a chemical intermediary can be omittedif the energy can from radicals from the gel precursor directly.

In some embodiments, initiation does not require a radiant energysource. For example, a polymer plug with free radicals can be introducedthrough one end of the tube. In this case, the polymer plug can beintroduced either before or after the monomer is drawn into the tube.Alternatively, initiator or facilitator can be introduced at only oneend of the tube. The requirement is that a polymer structure be formedin one section which extends only a fraction of the length in which gelis to be formed, while the remainder of the tube is essentially free ofpolymer.

Where polymer is not formed is as important as where it is formed. Theadvantages of the present invention arise from plug growth. If theinitial plug is as long as or nearly as long as the tube itself,longitudinal growth will be negligible. The initial plug should be atmost one-quarter the length of the tube. Generally, the initial plug isless than 10% of the tube length. Moreover, if multiple plugs areformed, monomer solution cannot fill the voids left as monomer trappedbetween plugs polymerizes. Hence, polymerization should be avoidedexcept within the initiation section and at the plug front.

Once the initial polymer structure is formed, it can serve as a seedwhich can grow by bonding with nearby monomer molecules. In thepreferred embodiments, polymerization progresses by moving the tuberelative to the same source used for initiation. However, in someembodiments a energy source different from the one used duringinitiation can be used for progressive polymerization. For example,photoinitiation can be followed by heat-supported progressivepolymerization.

Under particular circumstances polymerization can occur at the polymerfront without additional localized energy introduction. In such a case,an initiator source can be turned off and polymerization allowed toproceed. Alternatively, external energy can be applied to supportprogressive polymerization after physical introduction of a polymer seedstructure. In further alternatives, polymerization progresses due toprogression of a factor affecting polymerization. For example, heatconducted by a tube can be used to promote longitudinally progressivepolymerization, likewise, diffusion of an originally localized chemicalinitiator or facilitator can promote longitudinally progressivepolymerization.

In the preferred embodiments, the tube is moved past a localized energysource to promote progressive polymerization. Alternatively, the sourcecan be moved past a stationary tube. Movement can be virtual as well asphysical. For example, the heat or light source can be a linear array ofdiodes. Source movement is effected by selection of the diodes to beactivated at any given time. Similarly, a liquid crystal shutter can beused to select which sections of a tube are exposed by a light source.In other embodiments, a tube moves into, rather than past, an energysource. The source can be a heat or light tunnel. A tube can begradually inserted into the tunnel so that energy continues to be fedinto sections of tube introduced into the tunnel. This approach can bepreferred where polymerization behind the wavefront needs energy supportto complete polymerization or curing. In embodiments in whichpolymerization progresses without local energy introduction, there is norelative movement.

As described above, polymerization can be initiated near one end of thetube and polymerization progressed toward the other end. Someembodiments employing virtual movement of an energy source and some notrequiring a localized energy source to support polymer growth permitinitiation near the longitudinal center of the tube. Polymerization thenprogresses toward both ends at once. A energy source, such as aphoto-diode array, capable of virtual movement can be made to operate sothat two opposing illumination sequences drive polymerization towardboth ends of a tube at once. "Virtual" movement refers to apparentmovement caused by activating and deactivating energy sources insequence.

Monitoring polymerization is optional. Monitoring can be based onscattering or any other characteristic capable of monitoring anddistinguish a given polymer from its precursor. The feedback can be usedfor real-time control of progressive polymerization. In embodiments witha localized or tunnel energy source, feedback can be used to adjust thespeed of the relative movement of tube and source. In addition toadjusting speed, or instead of moving speed, other polymerization rateparameters can be adjusted. For example, temperature, ambient light,concentration of chemical initiator or facilitator, can be adjusted.Some of these variable are suitable for closed-loop regulation. Othersare more suitable to trial and error methodology in which the results ofone run are used to determine the settings for the next. These and othervariations upon and modifications to the described embodiments areprovided for by the present invention, the scope of which is limitedonly by the following claims.

I claim:
 1. A system for polymerization of a material in a tubecomprising:holding means for holding a longitudinally extending tubeassembly including said tube; an energy source capable of directingenergy into an initiation section of said tube to the exclusion of othersections of said tube; redirection means for progressively changing thesection of said tube into which said source directs radiation; monitormeans for monitoring the progress of polymerization in said tube; andcontrol means for controlling the rate of redirection relative to saidtube in response to the as-monitored progress of polymerization in saidtube, said control means being coupled to said first monitor means andsaid redirection means.
 2. A system as recited in claim 1 wherein saidenergy source includes an optical fiber along which electromagneticradiation can be directed to and through a wall of said tube.
 3. Asystem as recited in claim 2 wherein said monitor means includes asource of electromagnetic radiation including at least onecharacteristic wavelength not significantly radiated by said energysource, said monitor means including filter means for selectivelypassing said characteristic wavelength.
 4. A system as recited in claim1 wherein said energy source generates heat from a nichrome resistiveheating element.
 5. A system as recited in claim 1 further comprisingevaporation minimizing means for minimizing evaporation of said materialin said tube.
 6. A system as recited in claim 5 wherein said energysource radiates electromagnetic radiation via an optical fiber andthrough a wall of said tube.
 7. A system as recited in claim 6 whereinsaid monitor means includes a source of electromagnetic radiationincluding at least one characteristic wavelength not significantlyradiated by said energy source, said monitor means including filtermeans for selectively passing said characteristic wavelength.
 8. Asystem as recited in claim 5 wherein said energy source generates heatfrom a nichrome resistive heating element.
 9. A system as recited inclaim 1 further comprising a fluid reservoir disposed for receiving anentrance of said tube so that during said polymerization monomersolution can be drawn away from said entrance and toward a polymer frontin said tube.